Device and method for co-metering

ABSTRACT

A device for co-metering liquid and/or pasty products includes: a first metering unit for metering a first product; a second metering unit for metering a second product; and a nozzle including a first duct supplied by the first metering unit and opening out into a first orifice, a second duct supplied by the second metering unit and opening out into a second orifice, and a third duct opening out into a third orifice. The device is configured such that the third duct is supplied by the first and second metering units such that a mixture of the first and second products is discharged by the third orifice.

PRIORITY CLAIMS

This application is a divisional of U.S. application Ser. No. 15/114,270filed Jul. 26, 2016, which is a National Stage of InternationalApplication No. PCT/EP2014/077785 filed Dec. 15, 2014, which claimspriority to European Patent Application No. 14152622.8 filed Jan. 27,2014, the entire contents of which are incorporated herein by reference.

FIELD OF THE INVENTION

The present invention relates to a device and method for metering liquidand/or pasty products, in particular food products.

It more particularly relates to the field of metering several liquidand/or pasty products in order to fill a container with these products.The technique called “co-metering” consists of extruding severalproducts at the same time in order to fill a container therewith.

BACKGROUND

The general principle of co-metering is to supply a so-calledco-metering nozzle with several products produced via two or moremetering units. A metering unit for example includes a piston pumpsystem. The nozzle is used to discharge the doses of product in anorganized manner into the container.

In the field of food products, the co-metering of two or more productsin a container, typically transparent, is used more and more to give ashape and an attractive and new visual appearance to the product. Thistechnology is for example frequently used to fill containers of dairyproducts. Generally, this method is increasingly used in fresh dairydesserts packaged in transparent containers.

The co-metering for example makes it possible to give the finishedproduct (for example, a dessert in a container) a colored and contrastedvisual appearance. A difference in texture between the co-meteredproducts may also provide the consumer with a new gustatory experience.A successive introduction of different products in a container makes itpossible to obtain contrasting visual appearances and textures. However,the layers of different products are then superimposed on one anothersimply horizontally, which does not give the finished product aninnovative visual appearance. This is resolved by the simultaneousintroduction of several products during co-metering.

The general principles of co-metering are disclosed in document U.S.Pat. No. 3,267,971. In that document, the nozzle used has a shapespecific to the design (final appearance seen from outside thecontainer) that one wishes to obtain. The simplest design is a series ofvertical strips.

Other known devices allow a specific design, in particular when theproducts are dispensed via several ducts included by the nozzle. Thenozzle thus generally includes ducts opening into at least as manyorifices as there are co-metered products (typically two). These ductsmay be supplied continuously, sequentially or alternately. Document FR2,708,563 thus presents a co-metering device including a nozzle withmultiple ducts and orifices.

In order to give the finished product an attractive or originalappearance, it is known to create, during the co-metering of severalproducts, a relative vertical and/or rotational movement between thenozzle and the container that is filled. Thus, the nozzle and/or thecontainer may be set in motion. This makes it possible to obtainpatterns having a certain originality, such as zigzags or productssuperimposed on one another in a double helix.

This technique nevertheless has some number of technical difficulties.In general, the number of co-metered products is limited to two, andwith rare exceptions, three. Indeed, metering several products into acontainer involves supplying the packaging line with several differentproducts and requires the use of a metering and distribution systemspecific to each of those products. The more metering units there are,the more difficult it is to manage industrially the bulk related totheir juxtaposition, and the higher the overall design and productioncosts of the machine. That is why, although some machines are equippedwith two metering units, machines equipped with three units are muchrarer. The available space in certain packaging machines is also limitedand does not allow the juxtaposition of several metering units andnozzle holder tools.

SUMMARY

The developed invention seeks to obtain a device and a method forco-metering, making it possible to obtain a finished product includingat least three products with highly differentiated visual appearances ortextures, on a packaging line including a smaller number of meteringunits.

Thus, the invention pertains to a device for co-metering liquid and/orpasty products, including:

a first metering unit for metering a first product;

a second metering unit for metering a second product;

a nozzle including a first duct supplied by the first metering unit andopening into a first orifice, and a second duct supplied by the secondmetering unit and opening out into a second orifice. In such a deviceaccording to the invention, the nozzle includes a third duct openinginto a third orifice, the device being configured such that the thirdduct is supplied by the first and second metering units, such that amixture of the first and second products is discharged by said thirdorifice.

Thus, the mixture of the first and second products appears to be a thirdproduct, separate from the first and second products, in particular ifsaid first and second products have very different colors, shapes and/ortextures. The finished product which could be obtained using such adevice thus appears to include at least three products with clearlydifferentiated visual appearances or textures.

According to one embodiment, the device includes a third metering unit,connected to a fourth duct of the nozzle opening out near a fourthorifice. The nozzle may then advantageously include a fifth ductconnected to a fifth orifice, the device being configured such that thefifth duct is supplied by the third metering unit and the first meteringunit. The nozzle may further advantageously include a sixth ductconnected to a sixth orifice, the device being configured such that thesixth duct is supplied by the third metering unit and the secondmetering unit.

A device according to the invention may advantageously include a staticmixer configured so as to homogenize the mixture of the products comingfrom the two metering units.

The static mixer may be integrated into the nozzle. In other words, thenozzle may include the static mixer(s).

By gathering a maximum number of functions into the nozzle, such as themixing and the homogenization of the co-metered products, a very compactdevice may be obtained. Furthermore, a pre-existing production line mayeasily be adapted to obtain a device according to one embodiment of theinvention.

Preferably, the device includes means for sequentially supplying atleast one of the ducts of the nozzle.

The metering units may in particular each include a piston or eccentricrotor type pump.

The device may include a container holder and means suitable forcreating a relative movement between the nozzle and the containerholder. Such a relative movement, optionally conjugated with asequential supply of the ducts of the nozzle, allows the creation ofattractive or original patterns.

The nozzle may be movable. The container holder may be movable. Thenozzle and the container holder may both be movable. The notion ofmobility is to be understood here in a fixed plane of reference linkedto an element of the device fixed relative to the ground.

The invention also pertains to a method for co-metering liquid and/orpasty products, including the following steps:

providing a first product and a second product to a co-metering device;

simultaneously and/or sequentially discharging, into a container, via anozzle of the co-metering device including several orifices, the firstproduct through a first orifice of the nozzle, the second productthrough a second orifice of the nozzle, and a mixture of the first andsecond products through a third orifice of the nozzle.

The method may further comprise a step for homogenization of the mixtureof the first and second products, prior to the discharge of saidmixture.

Thus, at the end of the co-metering method, it is possible to obtain afinished product thus appearing to include at least three products withclearly differentiated visual appearances or textures.

Lastly, the invention relates to a product that may be obtained byimplementing the co-metering method for liquid and/or pasty products.

Other particularities and advantages of the invention will also appearin the following description, describing the invention in a generalcontext of co-metering.

BRIEF DESCRIPTION OF THE DRAWINGS

In the appended drawings, provided as non-limiting examples:

FIG. 1 diagrammatically shows a cross-sectional view of a nozzle withseveral orifices, as known in the state of the art;

FIG. 2 diagrammatically shows the face of the nozzle from FIG. 1 havingthe orifices;

FIG. 3 diagrammatically shows a finished product, as may be obtainedusing a co metering device implementing the nozzle shown in FIGS. 1 and2;

FIG. 4 diagrammatically shows the face having the orifices of a nozzleaccording to one known embodiment from the state of the art;

FIG. 5 diagrammatically shows a finished product, as it may be obtainedusing a co-metering device implementing the nozzle shown in FIG. 4;

FIG. 6 diagrammatically shows a co-metering device according to oneembodiment of the invention;

FIG. 7 diagrammatically shows the face bearing the orifices of a nozzleaccording to one embodiment of the invention;

FIGS. 8 and 9 diagrammatically show two finished products, as they mayrespectively be obtained using a co-metering device implementing thenozzle shown in FIG. 7;

FIG. 10 diagrammatically shows a first sectional view of a nozzle withseveral orifices, according to one embodiment of the invention;

FIG. 11 diagrammatically shows the face having the orifices of thenozzle shown in FIG. 10, and helps define the sectional view shown inFIG. 10;

FIG. 12 diagrammatically shows, according to a second sectional view,the nozzle shown in FIGS. 10 and 11;

FIG. 13 diagrammatically shows the face having the orifices of thenozzle shown in FIGS. 10, 11 and 12, and helps define the sectional viewshown in FIG. 12;

FIGS. 14 and 15 diagrammatically show two finished products, as they mayrespectively be obtained using a co-metering device implementing thenozzle shown in FIGS. 10 to 13;

FIGS. 16A and 16B diagrammatically show first and second sectionalviews, respectively, of the nozzle shown in FIG. 16C. FIG. 16Cdiagrammatically shows the face bearing the orifices of a nozzleaccording to one particular embodiment of the invention.

FIGS. 17 to 27 show examples of visual appearances of several finishedproducts in a transparent container, which may be obtained byco-metering contrasting products.

DETAILED DESCRIPTION

FIG. 1 diagrammatically shows, in sectional view along plane AA visiblein FIG. 2, a nozzle B with several orifices 11, 21, as known in thestate of the art, for discharging two liquid or pasty products so theymay be packaged in a container. The packaging may typically be done in acontainer that may be transparent or translucent.

FIG. 2 is a diagrammatic illustration of one face of the nozzle shown inFIG. 1, on which face several ducts open out forming the orifices 12, 22of the nozzle.

A first duct 1 opening into a first orifice 11 is intended to dispense afirst pasty or liquid product P1. A second duct 2 opening into a secondorifice 21 is intended to dispense a second product P2, pasty or liquid.

The first product P1 and second product P2 may be highly contrastedrelative to one another. The contrast may result from one or moreorganoleptic characteristics of the products P1 and P2, such as thecolor, taste, texture, viscosity, overrun, for example. In any case, thefirst product P1 and second product P2 are different from one another.Preferably, the first product P1 and the second product P2 are foodproducts, for example preparations used in dairy desserts.

As a non-limiting example, the first product P1 and the second productP2 are different from one another and selected from among:

primarily fruit-based preparations, such as puree, compote, coulis, orsyrup;

dairy preparations, optionally flavored, such as yogurt, fresh cheese,quark, cream;

pastry preparations, such as chocolate pudding, vanilla pudding,caramel, chocolate mousse, jellies.

For example and non-limitingly, the two products to be metered may be achocolate pudding and a vanilla pudding, a red fruit coulis and a freshcheese, or a white dairy mousse and a caramel coulis.

FIG. 3 diagrammatically shows a finished product, i.e., the productresulting from the co-metering of several pasty or liquid products in acontainer, typically transparent, as may be obtained using a co-meteringdevice implementing the nozzle shown in FIGS. 1 and 2. The example shownin FIG. 3 corresponds to the simplest appearance that the finishedproduct may have, i.e., with a distribution of the first product P1 andthe second product P2 side-by-side in the container, in equalquantities. The first orifice 11 and the second orifice 21 are shownhere with a round mouth. Any mouth shape may nevertheless be considereddepending on the final appearance desired for the product.

In general in the co-metering field, to avoid mixing different productsin the container and to distribute the co-metered products in thecontainer in the desired manner, a certain know-how is necessary.

Of course, one should have a good mastery of the metered and dispensedvolumes of the different pasty or liquid products, but it is also andabove all necessary to have good mastery of the flows of these differentproducts in the metering members and during the discharge through theorifices of the nozzle into the container.

For example, the discharge speed of these products must be controlledand reduced to avoid the mixing thereof.

The metering time imposed by the industrial machines also constitutes amajor constraint. Indeed, for better productivity, all of the meteringoperations must be done according to a short cycle, often shorter thantwo seconds, or even less than one second.

The mechanization of the metering is also a major industrial constraint,since the metering devices are commonly used on so-called multi-tracklines, i.e., on which several containers are filled at same time. Insuch industrial metering lines, generally 10 to 24 containers, or more,are metered at the same time. A metering device must therefore becompact, so that as many devices as there are containers to be filledcan be juxtaposed, over the containers, on the line.

Of course, more original appearances than that shown in FIG. 3 may beobtained, and various means and methods are known in the state of theart to do this. For example, instead of having two orifices, the nozzleB may have a larger number of orifices, as shown in FIG. 4. In practice,the nozzle B is configured so that each orifice discharges either thefirst product P1 or the second product P2. There is therefore, in thenozzle, a set of first ducts 1 opening into a set of first orifices 11,and a set of second ducts 2 opening into a set of second orifices 21.

According to the known embodiment from the state of the art and shown inFIG. 4, the nozzle B includes eight orifices arranged in a circle, suchthat one orifice intended to expel the product P1 is between two officesthat are directly adjacent to it and that are intended to expel thesecond product P2, and vice versa.

The appearance of the finished product, in a transparent container, ableto be obtained using the nozzle shown in FIG. 4, is shown in FIG. 5. Thefirst product P1 and second product P2 are distributed into as manyvertical sectors as the nozzle has orifices. In the case at hand, in theexample illustrated here, since the products are discharged in equalquantity by each orifice, the finished product in the container has foursectors of first product P1 alternating circularly with four sectors ofsecond product P2.

A helical stack of the products may also be obtained in a known mannerby rotating the container during its filling.

FIG. 6 diagrammatically shows a device for co-metering liquid and/orpasty products according to one embodiment of the invention.

The device includes a first metering unit 31 and a second metering unit32. The first and second metering units 41, 42 make it possible tointroduce a precise quantity of products into a container and preciselycontrol the flows of products.

The pieces of metering equipment most commonly used to control the flowsof products are positive pumps. The most appropriate one is based on thepiston principle.

The travel of the piston determines the volume to be metered and thedynamic axis thrust speed determines the dynamic aspiration andejection. It is in fact important to control the thrust and aspirationspeeds. The discharge speed makes it possible to manage the product flowat the outlet, and the aspiration speed allows correct stuffing of thepiston chamber with the product, which guarantees an appropriateregularity of the doses introduced upon each cycle. The aspiration speedmust nevertheless be controlled and adapted so as to avoid destructuringthe metered product.

Other types of pumps may also be used. So-called positive push pumps areparticularly appropriate. A positive pump works on the principle of anincrease followed by a decrease in the volume of the chamber. Amongpositive pumps, the following are known in particular: lobe pumps,sinusoidal pumps, membrane pumps, helical pumps. Typically, positivepumps of the eccentric rotor type may be used. Reference is commonlymade to Moineau-type pumps. These are particularly well suited tometering filled (including solid particles) and/or highly viscousproducts. Among positive pumps, so-called lobe or peristaltic pumps mayalso be used successfully for co-metering.

In a device according to the invention, the first metering unit 31 isconfigured to meter a first product P1. The device therefore makes itpossible to supply first product P1 of the first metering unit 41. Thesecond metering unit 42 is configured to meter a second product P2. Thedevice therefore allows the supply of second product P2 of the secondmetering unit 32.

The device includes a nozzle B for discharging products. The nozzleincludes a first duct 1 and a second duct 2, which are respectivelysupplied with a first product P1 by the first metering unit 41 and asecond product P2 by the second metering unit 42. In the invention, thenozzle includes a third duct 3. The first duct 1 opens out into a firstorifice 11 of the nozzle B, the second duct 2 opens out into a secondorifice 21 of the nozzle B, the third duct opens out into a thirdorifice 31 of the nozzle.

The third duct 3 is supplied by the first metering device 41 and by thesecond metering device 42, such that the third orifice discharges amixture M3 of the first and second products P1, P2. The mixture M3,inasmuch as the first product P1 and second product P2 are highlycontrasted, with different colors, and/or with clearly differentiatedtextures, may have a shade, a color and/or a texture very different fromthose of the first product P1 and second product P2, giving theimpression that it involves a third product strictly speaking.

The mixture M3 may be homogeneous or may be a partial mixture of thefirst product P1 and second product P2. The proportion of the firstproduct P1 and second product P2 may be adapted so as to obtain thedesired appearance or texture of the mixture M3.

Devices may be used to favor the proper mixing of the first product P1and second product P2. A static mixer 6 may be used. It may typically beinstalled in the third duct 3, or upstream from the third duct in aconduit supplied by the first and second metering units 41, 42.

The device described in FIG. 6 makes it possible to obtain a finishedproduct having the appearance diagrammatically shown in FIG. 8. Thefirst product P1, second product P2, and mixture M3 are distributed intothree vertical sectors.

By creating a relative movement between the nozzle B and the container5, it is possible to obtain more original or attractive appearances. Forexample, in the device shown in FIG. 6, the container is rotated by arotating holder 7 during its filling by the metering device. This makesit possible to obtain a finished product having the appearancediagrammatically shown in FIG. 9, i.e., having products stacked in atriple helix.

Many alternatives of the device shown in FIG. 6 can be designed withoutgoing outside the scope of the invention. Typically, the nozzle B mayhave more than three ducts and three orifices. Thus, the nozzle shown inFIG. 11 itself has eight orifices, in the case at hand two firstorifices 11 for discharging the first product P1, four second orifices21 for discharging the second product P2, and two third orifices 31 fordischarging the mixture M3. Furthermore, several alternatives of theinvention may be considered, in particular regarding how the third duct3 is created and supplied with products. For better compactness of theassembly and so as to be able to easily adapt a pre-existing lineprovided with only two metering unit, the mixture M3 may be formeddirectly in the third duct 3 of the nozzle B.

FIG. 10 thus shows, in a diagrammatic sectional view, a nozzle withseveral orifices 11, 21, 31, in the case at hand eight orifices,according to one embodiment of the invention. FIG. 10 indeed shows, withtwo section planes, along sector A-A′ shown in FIG. 11, so as to show inthe same figure a section plane passing through a first duct 1, and asection plane passing through a third duct 3.

FIG. 12 shows, in diagrammatic sectional view, the same nozzle as thatshown in FIGS. 10 and 11, along two section planes defined by the sectorC-C′ in FIG. 13. Thus, the same figure shows a section plane passingthrough a first duct 1 and a section plane passing through a second duct2.

The nozzle shown in FIGS. 10 to 13 is supplied with first product P1 andsecond product P2, respectively by a first metering unit 41 and a secondmetering unit 42, in two distinct stages of the nozzle. Each stageincludes a peripheral groove, i.e., a first peripheral groove 71 and asecond peripheral groove 72. Each first, second or third duct isrespectively supplied by a tapping in the first peripheral groove 71,the second peripheral groove 72, or in each of the first and secondperipheral grooves 71, 72.

The use of a nozzle as shown in FIGS. 10 to 13 makes it possible toobtain a finished product having the appearance diagrammatically shownin FIG. 14. The first product P1, second product P2 and mixture M3 aredispensed in as many vertical sectors as the nozzle has orifices, withthe distribution of the sectors defined by the distribution of theorifices of the nozzle B.

Through a relative rotational movement between the nozzle B and thecontainer 5, it is possible to have a finished product whose appearanceis shown in FIG. 15.

The first product P1, second product P2 and mixture M3 are stacked in aspiral,

according to the distribution of the orifices of the nozzle B.

According to another embodiment of the invention, the device may includea third metering unit for metering a third product. FIGS. 16A and 16Bshow, in diagrammatic sectional views, a nozzle with several orificesalong two section planes defined by the sectors D-D′ and E-E′ in FIG.16C. As shown in FIG. 16C a nozzle B including multiple orifices has, inaddition to a first orifice 11 for discharging a first product P1, asecond orifice for discharging a second product P2, a third orifice 31for discharging the mixture M3, a fourth orifice 81 for discharging thethird product. The third product then circulates in a fourth duct of thedevice, opening out into the fourth orifice 81.

According to various embodiments of the invention, several combinationsof the first, second and third products may be done to obtain as manymixtures with a unique shade, color and/or texture. Up to seven products(or mixtures) of different shades, colors and/or

textures may be provided by nozzle B when the co-metering deviceincludes three metering units each supplied with a different product: 1)a first product P1; 2) a second product P2; 3) a third product P3; 4) amixture M3 of the first product P1 and second product P2; 5) anothermixture of the first product P1 and third product P3; 6) another mixtureof the second product P2 and third product P3; 7) another mixture of thethree products.

In the example shown in FIG. 16, six products or mixtures may beprovided by the device: in addition to the aforementioned nozzleorifices, the nozzle has a fifth orifice 82 and a sixth orifice 83, thedevice being configured in the example illustrated here to expel amixture M4 of the first product P1 and third product P3 through thefifth orifice 82 and a mixture M5 of the second product P2 and thirdproduct P3 through a sixth orifice 83. FIG. 16A shows, with two sectionplanes, along sector D-D′ shown in FIG. 16C, a section plane passingthrough the first duct 1 that opens out into the first orifice 11 and asection plane passing through a fifth duct 92 that opens out into thefifth orifice 82. FIG. 16B shows, with two section planes, along sectorE-E′ shown in FIG. 16C, a section plane passing through the second duct2 that opens out into the second orifice 21 and a section plane passingthrough a sixth duct 93 that opens out into the sixth orifice 83.

In such a device configuration, each duct of the nozzle intended toexpel a mixture of several products may be equipped with mixing meanssuch as a static mixer.

The device may also include sequential supply means for at least one ofthe ducts. In other words, the device may include means for stopping andresuming, abruptly or gradually, the supply of certain ducts andtherefore the supply of products or mixtures by any one or more of theducts supplied via one of said sequential supply means. The sequentialsupply means may for example include means for driving appropriatemetering units. They may also or alternatively include dispensing valves8 (FIG. 6), for example solenoid valves, to interrupt the flow ofproduct (or mixture) in a given duct during the co-metering.

The developed invention therefore typically makes it possible to obtaina final product visually (or in terms of texture) appearing to includethree products, on a packaging line provided for metering only twoproducts, and equipped with only two metering units.

The invention is therefore applicable to the manufacture of manyproducts, in particular food products. For example, with vanilla puddingand dark chocolate pudding, it is possible to obtain a finished productappearing to include three separate products: vanilla pudding, milkchocolate pudding, and dark chocolate pudding. Likewise, with a whitecheese and red fruit coulis, it is possible to obtain a finished productappearing to contain a white cheese, a strawberry cheese, and beingmarbled with lines of red coulis. A white dairy mousse and caramel makesit possible to obtain a finished product showing a juxtaposition ofwhite mousse and chestnut caramel mousse, all striped with dark caramellines.

The invention thus developed makes it possible to obtain a aspectdiversity still unknown in the field, using relatively simple devices.By combining the invention with certain methods or know-how in the fieldof metering or co-metering liquid or pasty products, a wide variety ofinnovative or attractive aspects may be obtained. Certain parameterswhose mastery is important are described below, and various aspects orpatterns of the finished product that can be obtained by mastering theseparameters are shown in FIGS. 17 to 27.

The parameters pertain to taking into account characteristics of themetered product(s), the design of the metering devices, whether in termsof the general architecture, the choice of the metering technologies, orthe design of the nozzles, the control of the devices, and the controlof the relative position of the nozzle and the container filled duringthe metering.

The rheology of the products to be metered must be correctly taken intoaccount.

Indeed, a difference of viscosity or rheological behavior of theproducts to be metered increases the difficulty of co-metering. Manyrheological parameters need to be taken into account: the products maybe viscous or liquid, sticky or slippery, foamy or not, etc. Althoughtwo semi-viscous products with the same rheological behavior arerelatively easy to co-meter, the situation is more complex with a veryfluid product and a more viscous product, or when a very dense productis metered in a very airy mousse. A difference in density may in somesituations advantageously be used to separate two products. This is forexample the case of metering a caramel in a gelled milk, which settlesquickly at the bottom of the container.

To control the push and aspiration speeds, simple pneumatic pistons orsimple electric motors are not optimal. Motorization using automateddigital systems, using a servomotor system, is preferable. This makes itpossible to manage the accelerations and movement time of the movingelements of a pump (typically, the moving axis of a piston) to adaptthem to the characteristics of the metered products to obtain thedesired produced flow. Such motorization and management thereof byautomaton also makes it possible to synchronize each of the meteringunits. In the pushing of two products with highly different viscosities,it is for example appropriate to anticipate the pushing of the moreviscous one to obtain a simultaneous exit of both products from thenozzle nose.

An independent motorization of the pistons associated with each productquality is advantageously used.

The opening and closing times of the intake valves, and the dischargefrom the metering unit and the nozzle, will advantageously be drivenindependently from the pushing of a product by each metering unit.

Due to the quantity of parameters integrated into the controller, it ispreferable to develop clear procedures, typically for each productionoperator, and to provide safeguard and recall means for the adjustmentsof the metering devices. This makes it possible to obtain the desiredco-metering result reliably and repetitively.

Nevertheless, the old co-metering devices often implement a singlemotorization for a series of piston metering units, for example via ashared driving bar. One of the drawbacks of these devices lies in thepoor control of the volumes displaced from the various pistons. Indeed,the volume aspirated by a piston metering unit is sensitive to thepressure differences, even minimal, commonly observed in productdispensing systems. Yet with a single driving bar, no individualadjustment on a particular metering unit is possible, without changingthe adjustment of the other metering unit.

Additional systems may be used to offset this problem. For example, amechanical part may be added to allow an additional adjustment of thetravel of a piston. According to another system, the pressure lossexperienced by the product metered by a given metering unit is adaptedin order to compensate for the effect of the pressure differences on themetering.

One of the essential aspects to be controlled in the co-metering ofproducts is the flow speed of the metered products or mixtures. One ofthe key parameters influencing this aspect is the choice of diameters,shapes, section surfaces, hoses and ducts used, as well as the nozzleorifice. This then essentially involves adapting the flow speed bycalculating the proper passage section. This makes it possible to avoidshearing the product (which may lead to denaturing thereof) throughexcessive accelerations, and this may in some cases make it possible togive the metered product or mixture an energy useful for its orientationin the container during its discharge. Furthermore, to avoid mixing ofthe different co-metered products, it is desirable for the respectiveexit speeds of the products to remain relatively close. It is alsoimportant to make sure that the products remain in a laminar regime.Typically, a speed over 0.5 m/s most often causes an impact at thebottom of the container and a movement of the fluid that produces theirmixing. Generally 0.5 to 0.25 m/s constitute reasonable flow speeds forindustrial co-metering methods.

The applicant has further noted that modifications in the dynamics(speeds, accelerations) of the flow of products lead to a variety ofvisual aspects of the finished products.

Furthermore, the control of product flows is commonly disrupted byexcessive pressure losses. These pressure drops often depend on propermastery in terms of technical design of the device, well upstream fromthe metering nozzle. The choice of the diameters of the pipes and hosesis important, and depends on the viscosity of the various products. Itis also appropriate to reduce the elbows, valves, and other devices orconfigurations that are sources of pressure drops.

A different pressure drop experienced by each of the co-metered productsmay result in a non-simultaneous arrival of the products at the nozzleoutlet. It is then difficult to correctly master the exiting productflows.

Each metering unit of a metering or co-metering device is generallysupplied with products to be metered by a hopper. The variation of theproduct level in the hopper that supplies the various pieces of meteringequipment may have a negative impact on the regularity of the flow. Aregulated supply of the product to maintain a constant level in thehoppers is a positive factor to obtain a good regularity of the flow.

Furthermore, good mastery of the pressure in the same hoppers provides agreater consistency in the rest of the metering or co-metering method.Equipment for creating pressure and maintaining a constant pressure,typically by establishing an air overpressure in the hopper, may be usedto correctly control the pressure in the hopper. This is particularlyuseful and relevant when the metering or co-metering implementscompressible products, for example aerated products and foams.

The pressure losses upstream from the metering unit constitute animportant aspect. Indeed, an excessive pressure loss due to aninappropriate design of a duct (inadequate diameters, presence of manyelbows) between the hopper and the metering member(s) (piston pump, forexample) may negatively impact the result obtained downstream, andtherefore the metering quality. In a system including several meteringunits that each supply a nozzle, a disparity in the pressure lossesupstream from the metering unit causes a disparity in the volumesmetered by each of the metering units. Certain devices make it possibleto reduce the disparities or balance the pressure losses.

It is also possible to configure the device such that the metering unit,typically a piston metering unit, draws the metered product directly inthe hopper.

The pressure losses downstream from the metering unit constitute anotherimportant aspect. Indeed, the pressure losses may disrupt the properflow of the products. The distribution between the metering member andthe metering nozzle must tend to generate the smallest possible pressurelosses. The pressure losses are in particular related to the distancebetween the metering unit and the discharge nozzle, which is determinedby the general architecture of the metering device. To limit thepressure losses between the metering unit and the nozzle, one simplesolution comprises positioning the metering unit above, straight and asclose as possible to the nozzle and the containers. The generalcompactness of the device is therefore important.

However, such a solution is difficult to make compatible with a movablenozzle.

Furthermore, this configuration with metering units situated above thecontainers also complicates the design of so-called “hygienic” machines.

Indeed, in these ultra-clean packaging machines, where a laminar flow isused for hygienic reasons, it is preferable to offset the metering unitswith their moving parts outside the packaging enclosure (including thefilling line for containers). The metering pistons are thus often placedoutside the packaging enclosure to free space located perpendicular tothe containers to be packaged. Only the nozzles remain in the packagingenclosure, and are connected to metering unit by flexible and/or rigidpiping. This generates a significant pressure loss between the meteringunit and the nozzle.

The residual pressure upstream and downstream from the metering unit arealso influential parameters, mastery of which is important. If thepressure downstream from the metering unit is high, then there is abackflow of the product into the metering chamber during its loading(filling with product to be metered). This distorts the accurateknowledge of the volume actually aspirated, which typically does notcorrespond to the displacement of the pump. To minimize this phenomenon,the device may be equipped with a system of separating valves thatisolates the metering chamber from the zones immediately upstream ordownstream, during metering phases (aspiration or discharge). Valves ofthe rotary slide valve type may be used to that end.

In general, the metering devices that do not use a metering valveimmediately downstream from the metering unit and that have an offsetnozzle are relatively irregular and imprecise. In this configuration,the dead space of product at the end of metering, i.e., the residualvolume situated between the metering unit and the nozzle closing valve,is often much higher than the dose of product displaced and metered.

The residual pressure downstream from the metering unit is all the moreimportant when the metering is done at a fast pace, when the product isviscous and sticky, when the product is compressible and when thedownstream length of the piping is large. When one (or a combination) ofthese parameters causes a high residual pressure, there is a minimumtime necessary between the end of metering pushing and the return topressure equilibrium. This phenomenon is not favorable to a cleancut-off of the product at the outlet of the orifices of the nozzle, anddrips and runs may occur. In the case of metering a mousse, for example,the mousse dynamically compressed during the discharge operation tendsto expand between two metering cycles in the pipe connecting themetering unit to the discharge nozzle.

Furthermore, the flow of the viscous, sticky products or products whosevolume increases by overrun (called overrun products, such as whippedcream) are difficult to interrupt cleanly, in particular at the outletorifices of the nozzles. An expansion of the product after metering,runs caused by gravity may for example occur.

Several techniques exist to avoid this leakage, and quickly cancel anypressure in the nozzle orifices.

One of these techniques consists of making a cut in the discharge of theproduct by positioning a closing valve level with the dischargeorifices. Thus, there is no or practically no dead space, i.e., residualspace in the circuit between the closing valve and the dischargeorifice.

This simple solution on a device suitable for the injection of a singleproduct with a nozzle to a single orifice is difficult to implement whenthe nozzle is provided with multiple discharge orifices.

Some valve systems are configured to allow the simultaneous closing ofseveral discharge orifices. This is typically the case for flatmembranes, spherical membranes, complex machined gates, rotating platesand so-called “slide” systems.

The ease of cleaning these moving parts, their wear, sealing problems,and the bulk caused by adding these valves perpendicular to thecontainers to be filled may be elements making the application of such asystem particularly complex.

One technique to avoid runs consists of re-aspirating the product at theend of metering. This is done by creating a slightly negative pressurein the discharge orifice at the end of the metering cycle. This slightlower pressure may be created for example by equipping the circuit withtwo membrane valves (for example of the so-called “sleeve” membranetype), located upstream from the nozzle. To create the lower pressure,the two valves are closed simultaneously, then the valve furthestdownstream (closest to the discharge orifice) is reopened. This vacuummay alternatively be created by a specific product outlet which, byopening, makes it possible to rebalance the pressure in the circuit,causing a drop in the pressure upstream from the discharge orifice ofthe nozzle. A closure by sealing member assisted by a dual pneumaticsystem may also produce this lower pressure, one of the two pneumaticmembers causing a slight backward return of the sealing member aftercomplete closure. It is also possible to obtain the re-aspiration effectof the product just after the metering using a rotating closing gatehaving an appropriate design. In metering systems using positive rotarypumps, a brief backward return of the pump may also allow thisre-aspiration. Lastly, in systems implementing a motorization of thepistons by servomotors, this “respiration” can be done by simpleappropriate programming of the movement of the piston axis.

During the co-metering of several products, in addition to the dischargespeed of the products at the outlet of the orifices of the nozzle, theheight of the drop into the container is an important parameter to takeinto account to avoid the mixing of products and achieve a regularappearance in the container.

A constant maintenance of the position (height) of the nozzle withrespect to the surface of the products during their co-metering makes itpossible to form regular lines. This may be obtained using systems forraising the container on a packaging line using preformed containers, orusing a vertical displacement system for the nozzles on the machines. Inother words, either the container is moved with respect to the nozzle,or the nozzle is moved with respect to the container so as to maintain asubstantially constant drop height of the products. The systems formovement of the nozzle are particularly suitable when the packagingmachine used is of the type generally referred to as “Form Fill seal”,i.e., a machine that shapes the container that is filled, and seals it,and in particular a so-called “horizontal Form Fill seal” machine. Thedrop height is therefore an important parameter to obtain a finishedproduct with so-called vertical, or in quarters, metering as shown inFIGS. 3, 5, 8 and 14.

Conversely, it is possible to take advantage of the variation in thedrop height of the product to obtain certain aspects. Typically, bybringing the nozzle and the container farther away from or closer to oneanother several times during filling, a more or less random drop of theproducts is created. The products then organize themselves in inclinedor horizontal layers, and it is for example possible to obtain one ofthe aspects shown in FIGS. 17 and 18.

A slowing or interruption of the raising or lowering movement of thenozzle and/or container during the metering, associated with adiscontinuous flow of the products, makes it possible to obtain anaspect as shown in FIG. 19, meaning the aspect of a finished productincluding a product in which bubbles of another product are included. Amember 9 (FIG. 6), such as motorization of the type referred to as“brushless-servo”, provides great ease of controlling the relativemovement of the nozzle and the container or container holder.

Furthermore, a stop of the nozzle in an intermediate position in thecontainer makes it possible to finalize the surface of a co-meteredproduct by giving it a homogeneous aspect.

A slight contact between the outlet orifices and the product at the endof metering, followed by a rapid rising movement toward the upperposition, makes it possible to avoid runs and flows for stringy, viscousand sticky products (such as milk caramels, mousses, etc.).

For overrun products, such as whipped cream, for example, an appropriatecontrol of the movement of the nozzle relative to the container (or morespecifically relative to the level of product in the container) at theend of metering makes it possible to obtain a dome shape on the surfaceof the finished product.

For liquid products, driving the drop height also makes it possible, byexerting a movement opposite the drop of the product and by reducing thedrop as much as possible, to limit any splashing effect during the fallof the product, or any risk of mixing. This is in particular importantto obtain a gentle deposit of a liquid on a low viscosity product byminimizing the risk of mixing of the products.

Furthermore, the control of the drop height of the product, associatedwith appropriate control of the discharge dynamics of the product duringits metering, can also for example make it possible to position a secondproduct in a first product, at the desired depth in said first product.

Furthermore, in addition to imposing a vertical movement on the nozzleand/or the container, it is possible to impart a rotational movement tothe nozzle and/or the container to give the finished product a spiral orhelical aspect, as shown in FIGS. 9 and 15.

In large-capacity machines in which several containers are metered andfilled at the same time, several systems may be considered to performthis function, for example mechanical systems by gears or notched beltsfor the joint rotation of several containers. The systems used may inparticular be similar to the systems known in the field of decoratingindustrially produced pastries.

The rotation speed, which conditions the number of revolutions performedby the container or the nozzle during a metering cycle, makes itpossible to obtain a wide variety of spirals. A large number ofrevolutions, although difficult to obtain over the duration of ametering cycle, makes it possible to arrange the layers of co-meteredproducts nearly horizontally. The finished product then typically hasthe aspect shown in FIG. 20.

An alternation in the rotation direction during metering gives theproduct a zigzag spiraling aspect, as shown in FIG. 21.

The use of servomotors to control the rotation or elevation of thenozzle relative to the container makes it possible to finely vary theaccelerations, which further increases the variety of aspects that maybe obtained. It is for example possible to stretch a spiral verticallyby applying a variable speed during the elevation, or conversely tocreate wider contrasting zones by intermittently slowing the risingspeed of the nozzle.

The shape, section, number and position of the discharge orifices of thenozzle constitute parameters that all influence how the product will beorganized in the container.

A distribution of the orifices in a circle (at an equal distance fromthe center of the nozzle, considering the nozzle substantially having ashape of revolution) generally causes, during a simple verticalmetering, a geometric shape in sectors, with a straight separation ofthe products and spreading from the center toward the periphery of thecontainer. Such a distribution is shown in FIGS. 3, 5 and 8.

If the co-metered products have very different viscosities, it isappropriate, to obtain such regularly in the distribution of theproducts, to position the orifices respectively intended for thedischarge of each product at different distances from the center of thenozzle.

If one of the co-metered products is discharged through an orificesituated at the center of the nozzle, this product tends, during itsexpansion in the container, to push back the other product(s) toward theedges of the container, causing a striped distribution with a lateraldesign. The exact position of the orifices in order to obtain thedesired result, which depends on the dynamic viscosity of the product,is generally obtained and polished through successive trials.

Furthermore, if the section of the discharge orifices of one of theproducts is reduced to give that product a higher discharge speed thanthe other products, then that product will tend to organize itself in azigzag or in a striped manner in the container.

The discharge orifices of the different products may not be positionedin a single plane. This makes it possible, if applicable, to avoidcontact between the various products during and at the end of metering.Such contact would be contrary to obtaining a pronounced contrastbetween different products, due to local mixing.

On the contrary, it may be interesting to have the outlet orifices ofone of the products open out in the discharge orifice of a secondproduct, or slightly upstream from the discharge orifice of the otherproduct.

This causes a “gentle” or incomplete mixing of the two products,yielding a particular visual effect, for example marbled. Thehomogeneity of the mixture may be adjusted by using baffles placedinside the outlet ducts of said second product. The homogeneity of themixture may be increased by using a static mixer.

The material chosen to make up the nozzle also is important. The nozzlesare commonly made from stainless steel. Some plastics with a morehydrophobic behavior toward the products than stainless steel may alsobe used. Mixing different materials is also possible. Ceramic may alsobe used.

In order to obtain still other aspects of the finished products, it ispossible to shift, in time, the discharge phases of the doses ofdifferent products, which are therefore not all discharged entirelysimultaneously. It is thus possible to begin the discharge of a firstproduct followed by that of a second. The first product covers thebottom of the container, while the discharge of the second productbegins. One example aspect of a finished product thus obtained is shownin FIG. 22. The same principle is of course applicable to theco-metering of more than two products.

It is even possible, in the case where the discharge of the firstproduct is stopped when that of the second product begins, to organizethe products in superimposed layers.

If one of the products is metered in an alternating manner while anotheris metered continuously, an aspect having the form of spots may beobtained. The shape of the spots is also affected by the relativevertical movement between the nozzle and the container. Furthermore, thesecond product may also be distributed alternatingly in various ductswhose distribution makes it possible to obtain non-superimposed spots,as shown in FIGS. 23 and 24.

Furthermore, by gradually decreasing the flow of one discharged productwhile increasing the flow of a second product, the distribution of theproducts in the container may show a pyramidal shape, as shown in FIG.25, or a double, triple, etc. pyramidal shape as shown in FIG. 26.

The combination of the techniques previously set out makes it possibleto obtain finished products with a complex aspect, having attractivegeometric figures, like the finished product shown in FIG. 27.

It is also possible to use a thermostatically-controlled nozzle ormetering unit. Indeed, some products must be metered at a temperaturehigher than their solidification point. This is in particular the casefor chocolate or certain gels. The metering unit and/or nozzles are thenadvantageously temperature-regulated to avoid any clogging by solidifiedor thickened product. This is important in particular when the packagingline is stopped.

Furthermore, to keep the product at a substantially homogeneoustemperature or to avoid a phase separation, it is possible tocontinuously recirculate the product, which prevents it from stagnating.In this case, only part of the product that is circulating is thenmetered while another part, generally making up a large majority, isreturned toward the hopper.

As shown by the preceding description, a good mastery of co-meteringrequires the precise configuration and control of many parameters thatinteract with one another, such that obtaining a complete adjustmentachieving the desired result may prove complex. Typically, more than 20different parameters need to be adjusted and/or controlled to master thedischarge of the co-metered products, dynamically adapt the drop heightof the products, and if necessary, adapt the rotational movements. It istherefore preferable for all of the metering equipment to use ahigh-performing automation and a clear reading system for variousparameters, in particular intended for a production operator.

A set of parameters that make it possible to obtain the desired resultmay be saved. Such a set makes up a recipe. The recipe may in particularbe saved on digital storage means. A recipe may be called up by theelectronic control device of a metering or co-metering device. Based onsuch a recipe, a variation of one or more relevant parameters makes itpossible to obtain a complete array of attractive visual aspects.

The invention is claimed as follows:
 1. A device for co-metering liquid and/or pasty products, the device comprising: a first metering unit for metering a first product; a second metering unit for metering a second product; and a nozzle including a first duct supplied by the first metering unit and opening out into a first orifice, and the nozzle further including a second duct supplied by the second metering unit and opening out into a second orifice, the nozzle is configured to separately dispense the first product, the second product, and a mixture thereof out of the nozzle, and the nozzle further comprises a third duct opening out into a third orifice, the device being configured such that the third duct is supplied by the first and second metering units, such that a mixture of the first and second products is discharged by the third orifice.
 2. The device according to claim 1 comprising a third metering unit connected to a fourth duct of the nozzle, the fourth duct opening out into a fourth orifice.
 3. The device according to claim 2, wherein the nozzle comprises a fifth duct connected to a fifth orifice, the device being configured such that the fifth duct is supplied by the third metering unit and the first metering unit.
 4. The device according to claim 3, wherein the nozzle comprises a sixth duct connected to a sixth orifice, the device being configured such that the sixth duct is supplied by the third metering unit and the second metering unit.
 5. The device according to claim 1 comprising at least a static mixer configured to homogenize the mixture of the first product coming from the first metering unit and the second product coming from the second metering unit.
 6. The device according to claim 1, wherein the device is configured to sequentially supply at least one of the first, second, and third ducts of the nozzle.
 7. The device according to claim 1 comprising a container holder configured to generate a relative movement between the nozzle and the container holder.
 8. The device according to claim 7, wherein the nozzle is movable.
 9. The device according to claim 7, wherein the container holder is movable. 